Dry Composition Comprising an Extrusion Enhancer

ABSTRACT

Disclosed is a dry composition comprising one or more polyols, which upon addition of an aqueous medium forms a substantially homogenous paste suitable for use in haemostasis procedures. The paste reconstitutes spontaneously upon addition of the liquid; hence no mechanical mixing is required for said paste to form. The composition may further comprise an extrusion enhancer, such as albumin. Also disclosed are methods of preparing said dry composition, a paste obtained from said dry composition and uses of said dry composition or paste for medical and surgical purposes.

TECHNICAL FIELD

The present disclosure relates to a dry composition suitable for use in haemostasis and/or wound healing, wherein the dry composition comprises one or more polyols and forms a paste spontaneously upon addition of an aqueous medium. The composition further comprises an extrusion enhancer, such as albumin. The disclosure further relates to methods of preparing said dry composition and use of said composition.

BACKGROUND

Protein-based haemostatic materials such as collagen and gelatine are commercially available in solid sponge and loose or unpacked powder form for use in surgical procedures. Mixing of the loose or unpacked powder with a fluid such as saline or thrombin may form a paste or slurry that is useful as a haemostatic composition for use in cases of diffuse bleeding, particularly from uneven surfaces or hard to reach areas, depending on mixing conditions and relative ratios of the materials.

Conventional haemostatic pastes are prepared at the point of use by mechanical agitation and mixing of loose powder and liquid to provide uniformity of the composition. Mixing of the powder and fluid may be conducted in a container, such as a beaker. Such mixing requires transfer of the powder from its original container to the beaker, addition of the fluid to the beaker containing the powder, and then kneading of the mixture to form the paste. Only after the paste is thus formed may the paste be placed into a delivery means or applicator, e.g. a syringe, and applied to the wound.

WO 03/055531 relates to a container comprising a fixed amount of haemostatic agent in powder form, such as gelatine powder. Upon addition of a suitable amount of liquid, mechanical mixing within the container is performed by closing the lid and shaking the container. The resultant putty-like haemostatic paste can then be removed from the container and applied to a patient to promote haemostasis.

Alternately, attempts have been made to preload one syringe (Syringe I) with loose gelatine powder, and a second syringe (Syringe II) with liquid. When it is time to make a paste, Syringes I and II are connected via a luer lock and the solution in Syringe II is pushed into Syringe I. By attempting to pass the solution and powder repeatedly back and forth between Syringes I and II, a homogeneous paste may or may not be formed. Often in a surgical situation, a haemostatic paste with optimal powder:liquid ratio cannot be obtained due to insufficient mixing of the powder and the liquid in a syringe. Even if such methods of mixing are successful in forming a paste, the time and mechanical effort required to form the paste are undesirable or even unacceptable. Also the mixing can affect the final density of the paste (too intense mixing may result in a lower density paste) and hence inconsistent consistency of the paste from time to time.

Floseal Haemostatic Matrix (Baxter) is a kit for producing a haemostatic gelatine paste. The gelatine paste is produced by first making a thrombin solution and then transferring the gelatin matrix-thrombin solution mixture back and forth between two connected syringes for a total of at least twenty passes. The paste can then be applied to a patient to promote haemostasis directly from the syringe.

Likewise, Surgiflo® Haemostatic Matrix (Ethicon) is a kit for producing a haemostatic gelatine paste comprising thrombin, which is prepared by transferring the gelatin matrix-thrombin solution mixture back and forth between two connected syringes for a total of at least 6 passes.

US 2005/0284809 relates to a method for preparing a haemostatic paste that more readily absorbs aqueous liquids, such that less mechanical force and time is required in order to form a flowable haemostatic paste. The paste of US 2005/0284809 is prepared from compressed haemostatic powder particles and to prepare the paste, it must be transferred back and forth between connected syringes for a total of at least 5 passes.

WO 2011/151400 relates to a process for making a dry haemostatic composition comprising a coagulation inducing agent such as thrombin and a biocompatible polymer such as gelatine. The coagulation inducing agent and the biocompatible polymer are mixed to form a paste and the paste is subjected to lyophilisation. The resulting dry composition is reconstituted by transferring the composition and a diluent back and forth between two connected syringes for a total of at least twenty passes as described previously.

Mixing procedures and manipulations are time consuming and may potentially compromise the sterility of the haemostatic paste. It would be desirable if a haemostatic composition could be provided which would eliminate the need for such undesirable mixing requirements.

WO 2013/185776 discloses a dry paste composition suitable for wound healing and haemostatic use which reconstitutes spontaneously to form a flowable paste, i.e. without any mixing required, upon addition of an aqueous medium. The dry composition is prepared by mixing a crosslinked biocompatible polymer, one or more polyols and an aqueous medium to prepare a paste and then lyophilising the paste to obtain the dry composition.

WO 2013/060770 discloses a gelatine paste composition, wherein said composition comprises an extrusion enhancer. It is shown that the provision of extrusion enhancers, such as albumin, in the appropriate amount, enables the use of higher gelatine concentrations which may in turn improve the haemostatic properties of such products. WO 2013/060770 is incorporated by reference in its entirety.

It would be desirable to provide spontaneously reconstituting dry paste compositions which are easier to extrude from a syringe than conventional flowable paste products. It would also be desirable to provide spontaneously reconstituting dry paste compositions having a higher concentration of polymer, e.g. gelatine, than conventional flowable pastes, with a retained ability to be extruded easily from a syringe.

SUMMARY

The present disclosure relates to an improved dry composition, which upon addition of an adequate amount of an aqueous medium forms a substantially homogenous paste suitable for use in haemostasis and wound healing procedures. The paste forms spontaneously upon addition of the liquid, i.e. no mechanical mixing is required for said paste to form.

The disclosure further relates to a method of preparing said dry composition comprising the steps of:

-   -   a. providing a biocompatible polymer in powder form, one or more         polyols, an extrusion enhancer and an aqueous medium,     -   b. mixing the biocompatible polymer, the one or more polyols,         the extrusion enhancer and the aqueous medium to obtain a paste,         and     -   c. drying the paste.

The biocompatible polymer is preferably suitable for use in haemostasis and/or wound healing.

Preferably, the extrusion enhancer is albumin, more preferred human serum albumin.

Uses of the paste formed from the dry composition are likewise covered by the present disclosure.

DESCRIPTION OF DRAWINGS

FIG. 1. Phase diagram of water. The phase diagram shows, in pressure-temperature space, the lines of equilibrium or phase boundaries between the three phases of solid, liquid, and gas.

FIG. 2. Average reconstitution time +/−standard deviation of the freeze-dried gelatine pastes comprising different polyols of example 6.

DEFINITIONS

A “bioactive agent” is any agent, drug, compound, composition of matter or mixture which provides some pharmacologic, often beneficial, effect that can be demonstrated in vivo or in vitro. An agent is thus considered bioactive if it has interaction with or effect on a cell tissue in the human or animal body. As used herein, this term further includes any physiologically or pharmacologically active substance that produces a localized or systemic effect in an individual. Bioactive agents may be a protein, such as an enzyme. Further examples of bioactive agents include, but are not limited to, agents comprising or consisting of an oligosaccharide, a polysaccharide, an optionally glycosylated peptide, an optionally glycosylated polypeptide, an oligonucleotide, a polynucleotide, a lipid, a fatty acid, a fatty acid ester and secondary metabolites. It may be used either prophylactically, therapeutically, in connection with treatment of an individual, such as a human or any other animal.

“Biocompatible” refers to a material's ability to perform its intended function without eliciting any undesirable local or systemic effects in the host.

“Biologically absorbable” is a term which in the present context is used to describe that the materials of which the said powder are made can be degraded in the body to smaller molecules having a size which allows them to be transported into the blood stream. By said degradation and absorption the said powder materials will gradually be removed from the site of application. For example, gelatine can be degraded by proteolytic tissue enzymes to absorbable smaller molecules, whereby the gelatine when applied in tissues typically is absorbed within about 4-6 weeks and when applied on bleeding surfaces and mucous membranes typically within 3-5 days.

“Extrusion enhancer” according to the present disclosure covers any biocompatible compound capable of facilitating extrusion of a paste from a syringe.

A “gel” is a solid, jelly-like material that can have properties ranging from soft and weak to hard and tough. Gels are defined as a substantially dilute cross-linked system, which exhibits no flow when in the steady-state. By weight, gels are mostly liquid, yet they behave like solids due to a three-dimensional cross-linked network within the liquid. It is the crosslinks within the fluid that give a gel its structure (hardness) and contribute to stickiness (tack). In this way gels are a dispersion of molecules of a liquid within a solid in which the solid is the continuous phase and the liquid is the discontinuous phase. A gel is not a paste or slurry.

“Haemostasis” is a process which causes bleeding to diminish or stop. Haemostasis occurs when blood is present outside of the body or blood vessels and is the instinctive response for the body to stop bleeding and loss of blood. During haemostasis three steps occur in a rapid sequence. Vascular spasm is the first response as the blood vessels constrict to allow less blood to be lost. In the second step, platelet plug formation, platelets stick together to form a temporary seal to cover the break in the vessel wall. The third and last step is called coagulation or blood clotting. Coagulation reinforces the platelet plug with fibrin threads that act as a “molecular glue”.

A “haemostatic agent” according to the present disclosure is a biologically absorbable material. Examples of suitable biologically absorbable materials include but are not limited to gelatine, collagen, chitin, chitosan, alginate, cellulose, polyglycolic acid, polyacetic acid and mixtures thereof.

“International Unit (IU)”. In pharmacology, the International Unit is a unit of measurement for the amount of a substance, based on biological activity or effect. It is abbreviated as IU, UI, or as IE. It is used to quantify vitamins, hormones, some medications, vaccines, blood products, and similar biologically active substances.

A “paste” according to the present disclosure has a malleable, putty-like consistency, such as toothpaste. A paste is a thick fluid mixture of pulverized solid/solid in powder form with a liquid. A paste is a substance that behaves as a solid until a sufficiently large load or stress is applied, at which point it flows like a fluid, i.e. a paste is flowable. Pastes typically consist of a suspension of granular material in a background fluid. The individual grains are jammed together like sand on a beach, forming a disordered, glassy or amorphous structure, and giving pastes their solid-like character. It is this “jamming together” that gives pastes some of their most unusual properties; this causes paste to demonstrate properties of fragile matter. A paste is not a gel/jelly. A “slurry” is a fluid mixture of a powdered/pulverized solid with a liquid (usually water). Slurries behave in some ways like thick fluids, flowing under gravity and being capable of being pumped if not too thick. A slurry may be regarded as a thin paste, i.e. a slurry generally contains more water than a paste.

“Percentage”. If nothing else in indicated, the percentage is w/w.

“Spontaneous”. The term “spontaneous” is used to describe phenomena arising from internal forces or causes, which are independent of external agencies or stimuli and which happen within a short period of time, i.e. preferably within less than about 30 seconds, more preferred within less than about 20 seconds, even more preferred within less than about 10 seconds or within less than about 5 seconds.

DETAILED DESCRIPTION

The present disclosure relates to a dry composition, which upon addition of an adequate amount of an aqueous medium forms a substantially homogenous paste suitable for use in haemostasis procedures. The paste forms spontaneously upon addition of the liquid component, i.e. no mechanical mixing is required for said paste to form.

The dry composition may be prepared by a method comprising the sequential steps of:

-   -   a. providing a biocompatible polymer in powder form, one or more         polyols, an extrusion enhancer and an aqueous medium,     -   b. mixing the biocompatible polymer, the one or more polyols,         the extrusion enhancer and the aqueous medium to obtain a paste,         and     -   c. drying the paste.

The present disclosure further relates to a paste suitable for use in haemostasis and/or wound healing procedures prepared by adding an aqueous medium to the dry composition and use of said paste for promoting haemostasis and/or wound healing.

Disclosed is also use of the dry composition as described herein in the preparation of a paste for use in haemostatic and wound healing procedures.

The advantages of the dry composition disclosed herein are numerous and include:

-   -   Less time spent preparing the paste, e.g. bleeding can be         stopped faster.     -   Decreased risk of compromising the sterility of the paste during         preparation due to less handling steps.     -   Decreased risk of making mistakes during preparation due to the         simplified preparation of the paste.     -   Optimal consistency of paste obtained every time.     -   Facile extrusion of paste (less force needed to expel the         haemostatic paste from e.g. a syringe) and thus increased         accuracy of application of the haemostatic paste.     -   Bioactive agents, which are unstable in solution may be added to         the paste prior to drying and will thus be present in the dry         composition of the disclosure. For example, thrombin may be         added to the paste prior to drying, thereby avoiding the         time-consuming and error-prone thrombin dilution steps.

All of the above factors lead to increased patient safety.

Biocompatible Polymer

The present disclosure relates to a biocompatible agent in powder form, which is used to create a paste. The paste is then dried to obtain a dry composition suitable for use in haemostasis and wound healing procedures.

The biocompatible polymer of the present disclosure may be a biologic or a non-biologic polymer. Suitable biologic polymers include proteins, such as gelatin, soluble collagen, albumin, hemoglobin, casein, fibrinogen, fibrin, fibronectin, elastin, keratin, and laminin; or derivatives or combinations thereof. Particularly preferred is the use of gelatin or soluble non-fibrillar collagen, more preferably gelatin. Other suitable biologic polymers include polysaccharides, such as glycosaminoglycans, starch derivatives, xylan, cellulose derivatives, hemicellulose derivatives, agarose, alginate, and chitosan; or derivatives or combinations thereof. Suitable non-biologic polymers will be selected to be degradable by either of two mechanisms, i.e. (1) break down of the polymeric backbone or (2) degradation of side chains which result in aqueous solubility. Exemplary nonbiologic polymers include synthetics, such as polyacrylates, polymethacrylates, polyacrylamides, polyvinyl resins, polylactide-glycolides, polycaprolactones, and polyoxyethylenes; or derivatives or combinations thereof. Also combinations of different kinds of polymers are possible.

The paste of the present disclosure may either comprise a single biocompatible polymer or a mixture of two or more biocompatible polymers.

In one embodiment, the biocompatible polymer is biologically absorbable. Examples of suitable biologically absorbable materials include gelatine, collagen, chitin, chitosan, alginate, cellulose, oxidised cellulose, polyglycolic acid, polyacetic acid and combinations thereof. It will be understood that various forms thereof, such as linear or cross-linked forms, salts, esters and the like are also contemplated for the present disclosure.

In a preferred embodiment of the disclosure, the biologically absorbable material is gelatine. Gelatine is preferred since gelatine is highly biologically absorbable. Furthermore, gelatine is highly biocompatible, meaning that it is non-toxic to an animal, such as a human being, when/if entering the blood stream or being in long-term contact with human tissues.

The gelatine typically originates from a porcine source, but may originate from other animal sources, such as from bovine or fish sources. The gelatine may also be synthetically made, i.e. made by recombinant means.

In a preferred embodiment the polymer is cross-linked.

Any suitable cross-linking methods known to a person of skill may be used including both chemical and physical cross-linking methods.

In one embodiment of the present disclosure the polymer has been cross-linked by physical means, such as by dry heat. The dry heat treatment is usually performed at temperatures between 100° C. and 250° C., such as about 110° C. to about 200° C. In particular the temperature may be in the range of 110-160° C., e.g. in the range of 110-140° C., or in the range of 120-180° C., or in the range of 130-170° C., or in the range of 130-160° C., or in the range of 120-150° C. The period of time for cross-linking may be optimised by a skilled person and is normally a period between about 10 minutes to about 12 hours, such as about 1 hour to about 10 hours, for example between about 2 hours to about 10 hours, such as between about 4 hours to about 8 hours, for example between about 5 hours to about 7 hours, such as about 6 hours.

Examples of suitable chemical cross-linking agents include but are not limited to aldehydes, in particular glutaraldehyde and formaldehyde, acyl azide, caboiimides, hexamethylene diisocyanate, polyether oxide, 1,4-butanedioldiglycidyl ether, tannic acid, aldose sugars, e.g. D-fructose, genipin and dye-mediated photo-oxidation. Specific compounds include but are not limited to I-(3-dimethylaminopropyl)-3-ethylcarboiimide hydrochloride (EDC), dithiobis(propanoic dihydrazide) (DTP), I-ethyl-3-(3-dimethylamino-propyl)-carbodiimide (EDAC).

In one embodiment the biocompatible polymer in powder form is obtained from a cross-linked sponge. The biocompatible polymer may for example be obtained from cross-linked sponges of gelatine or collagen, in particular cross-linked sponges of gelatine (such as the commercially available Spongostan® sponges and Surgifoam® sponges). The cross-linked sponges are micronised by methods known in the art to obtain a cross-linked biocompatible polymer in powder form, such as by rotary bed, extrusion, granulation and treatment in an intensive mixer, or milling (e.g. by using a hammer mill or a centrifugal mill).

Spongostan®/Surgifoam® available from Ethicon is a gelatine based cross-linked absorbable haemostatic sponge. It absorbs >35 g of blood/g and within 4-6 weeks it is completely absorbed in the human body.

The cross-linked powder particles are in one embodiment less than approximately 1000 microns in size, i.e. so that they are able to pass through a 1×1 mm sieve.

In one embodiment, the paste prior to drying comprises between about 10% to about 60% of the biocompatible polymer, for example about 10% to about 50% of the biocompatible polymer, such as about 10% to about 40% of the biocompatible polymer, for example about 10% to about 30% of the biocompatible polymer, such as about 12% to about 25% of the biocompatible polymer, for example about 14% to about 25% of the biocompatible polymer, such as about 15% to about 25% of the biocompatible polymer, for example about 16% to about 20% of the biocompatible polymer, such as about 17% to about 20% of the biocompatible polymer, for example about 18% to about 20% of the biocompatible polymer.

In one embodiment, the paste prior to drying comprises more than 10% of the biocompatible polymer, such as more than 15% of the biocompatible polymer, for example more than 16% of the biocompatible polymer, such as more than 17% of the biocompatible polymer, for example more than 18% of the biocompatible polymer, such as more than 19% of the biocompatible polymer, for example more than 20% of the biocompatible polymer.

In one embodiment, the paste prior to drying comprises less than 40% of the biocompatible polymer, such as less than 30% of the biocompatible polymer, for example less than 25% of the biocompatible polymer, such as less than 20% of the biocompatible polymer.

In a preferred embodiment, the paste prior to drying comprises between about 10% to about 30% of the biocompatible polymer, more preferred between about 15% to about 25% of the biocompatible polymer, such as about 20% of the biocompatible polymer.

In one embodiment, the paste prior to drying comprises between about 15% to about 20% of the biocompatible polymer, such as between about 16% to about 20% of the biocompatible polymer, for example between about 17% and about 20% of the biocompatible polymer, such as between about 18% to about 20% of the biocompatible polymer.

In one embodiment, the paste prior to drying comprises between about 20% to about 25% of the biocompatible polymer, such as between about 21% to about 25% of the biocompatible polymer, for example between about 22% and about 25% of the biocompatible polymer, such as between about 23% to about 25% of the biocompatible polymer.

After drying, the composition comprises between about 40% and 80% of the biocompatible polymer, such as between about 45% and 80% of the biocompatible polymer, for example between about 50% and 80% of the biocompatible polymer, such as between about 55% and 80% of the biocompatible polymer.

In one embodiment, the composition after drying comprises between about 40% and 80% of the biocompatible polymer, such as between about 45% and 75% of the biocompatible polymer, for example between about 50% and 70% of the biocompatible polymer.

In one embodiment, the dry composition of the present disclosure comprises more than about 30% of the biocompatible polymer, such as more than about 40% of the biocompatible polymer, for example more than about 45% of the biocompatible polymer, such as more than about 50% of the biocompatible polymer, for example more than about 55% of the biocompatible polymer, such as more than about 60% of the biocompatible polymer, for example more than about 65% of the biocompatible polymer, such as more than about 70% of the biocompatible polymer, for example more than about 75% of the biocompatible polymer, such as more than about 80% of the biocompatible polymer.

In one embodiment, the dry composition of the present disclosure comprises less than about 80% of the biocompatible polymer, such as less than about 70% of the biocompatible polymer, for example less than about 65% of the biocompatible polymer, such as less than about 60% of the biocompatible polymer, for example less than about 55% of the biocompatible polymer, such as less than about 50% of the biocompatible polymer.

Aqueous Medium

The aqueous medium of the present disclosure may be any aqueous medium suitable for preparing a paste suitable for haemostatic use known to a person of skill, e.g. water, saline, a calcium chloride solution or a buffered aqueous medium. The water may be WFI (Water For Injection). The aqueous medium is selected so that the tonicity of the reconstituted paste product is suitable for use on a human or animal subject.

The aqueous medium of the present disclosure is in one embodiment a saline solution.

The aqueous medium of the present disclosure is in one embodiment a calcium chloride solution.

In other embodiments, the aqueous medium is water.

The aqueous medium may also be a buffered aqueous medium suitable for use in a haemostatic paste. Any suitable buffering agent known to a person of skill may be used, such as one or more buffering agents selected from the group consisting of: Sodium citrate; Citric acid, Sodium citrate; Acetic acid, Sodium acetate; K2HPO4, KH2PO4; Na2HPO4, NaH2PO4; CHES; Borax, Sodium hydroxide; TAPS; Bicine; Tris; Tricine; TAPSO; HEPES; TES; MOPS; PIPES; Cacodylate; SSC; MES, or others. The pH of the buffered aqueous medium should be suitable for creating a haemostatic paste intended for human use and can be determined by the skilled person.

The amount of aqueous medium is adjusted to the amount of biocompatible polymer so that a paste of a suitable consistency forms. To optimise manufacturing, it may in some instances be desirable to add less water to the paste prior to drying than is desired in the final reconstituted paste composition so that the paste takes up as little space as possible and less energy is required to remove water in the drying step. The paste prior to drying may thus have lower water content than the final reconstituted paste. The “missing” water can be added during reconstitution to obtain a flowable paste having a desired water:biocompatible polymer ratio.

The paste of the present disclosure prior to drying comprises between about 50% and about 90% of water, such as between about 55% and about 85% of water, for example between about 60% and about 80% of water, such as about 70% of water.

Preferably, the paste of the present disclosure prior to drying comprises between about 60% and about 80%, more preferred about 70% to about 75% of water.

After drying, the dry composition comprises less than about 5% of water, such as less than about 3% of water, preferably less than about 2% of water, more preferred less than about 1.5% of water, even more preferred less than about 1% of water or even less. Hence, in one embodiment, the dry composition comprises from about 0.1 to about 5% water, such as from about 0.1% to about 2% water.

In one embodiment, the residual water content in the dry composition is about 0.5% or less. Such a low residual water content is possible with e.g. industrial freeze-drying apparatuses.

A low residual water content in the composition after drying is desirable as it decreases the risk of microbial growth in the dry composition. Furthermore, a low residual water content is essential if the composition comprises bioactive agents that are unstable in aqueous conditions, such as e.g. thrombin. If thrombin is present in the composition of the present disclosure, the residual water content in the dry composition is preferably less than about 3% water, more preferred less than about 2% water.

Polyols

According to the present disclosure, one or more polyols are added to the composition prior to drying the composition. The one or more polyols play a role in achieving a dry composition which upon addition of a liquid in the form of an aqueous medium such as water spontaneously reconstitutes to form a paste of an optimal consistency for haemostatic purposes without the use of mechanical mixing or stirring of any kind.

A polyol as defined herein is a compound with multiple hydroxyl functional groups. Polyols as defined herein include sugars (mono-, di- and polysaccharides) and sugar alcohols and derivatives thereof.

Monosaccharides include but are not limited to glucose, fructose, galactose, xylose and ribose.

Disaccharides include but are not limited to sucrose (saccharose), lactulose, lactose, maltose, trehalose and cellobiose.

Polysaccharides include but are not limited to starch, glycogen, cellulose and chitin.

A sugar alcohol, also known as a polyalcohol is a hydrogenated form of carbohydrate, whose carbonyl group (aldehyde or ketone, reducing sugar) has been reduced to a primary or secondary hydroxyl group (hence the alcohol). Sugar alcohols have the general formula H(HCHO)_(n+1)H, whereas sugars have H(HCHO)_(n)HCO. Some common sugar alcohols which may be used in the method of the present disclosure include but are not limited to: Glycol (2-carbon), Glycerol (3-carbon), Erythritol (4-carbon), Threitol (4-carbon), Arabitol (5-carbon), Xylitol (5-carbon), Ribitol (5-carbon), Mannitol (6-carbon), Sorbitol (6-carbon), Dulcitol (6-carbon), Fucitol (6-carbon), Iditol (6-carbon), Inositol (6-carbon; a cyclic sugar alcohol), volemitol (7-carbon), Isomalt (12-carbon), Maltitol (12-carbon), Lactitol (12-carbon), Polyglycitol.

In one embodiment, the composition comprises a single polyol.

In one embodiment of the disclosure, the composition comprises more than one polyol, such as two, three, four, five, six or even more different polyols.

In one embodiment of the disclosure, the composition comprises two polyols, for example mannitol and glycerol or trehalose and a glycol.

In one embodiment of the disclosure, the composition comprises one or more sugar alcohols, such as one or more sugar alcohols selected from the group consisting of Glycol, Glycerol, Erythritol, Threitol, Arabitol, Xylitol, Ribitol, Mannitol, Sorbitol, Dulcitol, Fucitol, Iditol, Inositol, volemitol, Isomalt, Maltitol, Lactitol and Polyglycitol.

In one embodiment, the composition comprises one or more sugar alcohols and one or more sugars, such as one sugar alcohol and one sugar.

In one embodiment, the composition comprises one sugar alcohol and optionally one or more additional polyols, which may be either sugar alcohols or sugars.

In one embodiment, the composition does not comprise a sugar as the only polyol.

In one embodiment of the disclosure, the composition comprises mannitol.

In one embodiment of the disclosure, the composition comprises sorbitol.

In one embodiment of the disclosure, the composition comprises glycerol.

In one embodiment of the disclosure, the composition comprises trehalose.

In one embodiment of the disclosure, the composition comprises glycol, such as propylene glycol.

In one embodiment of the disclosure, the composition comprises xylitol.

In one embodiment of the disclosure, the composition comprises maltitol.

In one embodiment of the disclosure, the composition comprises sorbitol.

In one embodiment the paste prior to drying comprises from about 1% to about 40% of one or more polyols, for example from about 1% to about 30% of one or more polyols, such as from about 1% to about 25% of one or more polyols, for example from about 1% to about 20% of one or more polyols, such as from about 1% to about 15% of one or more polyols, such as from about 1% to about 14% of one or more polyols, for example from about 1% to about 13% of one or more polyols, such as from about 1% to about 12% of one or more polyols, for example from about 1% to about 11% of one or more polyols, such as about 1% to about 10% of one or more polyols.

In one embodiment the paste prior to drying comprises from about 2% to about 40% of one or more polyols, for example from about 2% to about 30% of one or more polyols, such as from about 2% to about 25% of one or more polyols, for example from about 2% to about 20% of one or more polyols, such as from about 2% to about 18% of one or more polyols, for example from about 2% to about 17% of one or more polyols, such as from about 2% to about 16% of one or more polyols, for example from about 2% to about 15% of one or more polyols, such as from about 2% to about 14% of one or more polyols, for example from about 2% to about 13% of one or more polyols, such as from about 2% to about 12% of one or more polyols, for example from about 2% to about 11% of one or more polyols, such as about 2% to about 10% of one or more polyols.

In one embodiment the paste prior to drying comprises from about 3% to about 40% of one or more polyols, for example from about 3% to about 30% of one or more polyols, such as from about 3% to about 25% of one or more polyols, for example from about 3% to about 20% of one or more polyols, such as from about 3% to about 18% of one or more polyols, for example from about 3% to about 17% of one or more polyols, such as from about 3% to about 16% of one or more polyols, for example from about 3% to about 15% of one or more polyols, such as from about 3% to about 14% of one or more polyols, for example from about 3% to about 13% of one or more polyols, such as from about 3% to about 12% of one or more polyols, for example from about 3% to about 11% of one or more polyols, such as about 3% to about 10% of one or more polyols.

In one embodiment, the paste prior to drying comprises more than about 5% of one or more polyols, hence in one embodiment the paste prior to drying comprises from about 5% to about 40% of one or more polyols, for example from about 5% to about 30% of one or more polyols, such as from about 5% to about 25% of one or more polyols, for example from about 5% to about 20% of one or more polyols, such as from about 5% to about 18% of one or more polyols, for example from about 5% to about 17% of one or more polyols, such as from about 5% to about 16% of one or more polyols, for example from about 5% to about 15% of one or more polyols, such as from about 5% to about 14% of one or more polyols, for example from about 5% to about 13% of one or more polyols, such as from about 5% to about 12% of one or more polyols, for example from about 5% to about 11% of one or more polyols, such as about 5% to about 10% of one or more polyols.

In one embodiment the paste prior to drying comprises from about 6% to about 40% of one or more polyols, for example from about 6% to about 30% of one or more polyols, such as from about 6% to about 25% of one or more polyols, for example from about 6% to about 20% of one or more polyols, such as from about 6% to about 18% of one or more polyols, for example from about 6% to about 17% of one or more polyols, such as from about 6% to about 16% of one or more polyols, for example from about 6% to about 15% of one or more polyols, such as from about 6% to about 14% of one or more polyols, for example from about 6% to about 13% of one or more polyols, such as from about 6% to about 12% of one or more polyols, for example from about 6% to about 11% of one or more polyols, such as about 6% to about 10% of one or more polyols.

In one embodiment the paste prior to drying comprises from about 10% to about 40% of one or more polyols, for example from about 10% to about 30% of one or more polyols, such as from about 10% to about 25% of one or more polyols, for example from about 10% to about 20% of one or more polyols, such as from about 10% to about 18% of one or more polyols, for example from about 10% to about 17% of one or more polyols, such as from about 10% to about 16% of one or more polyols, for example from about 10% to about 15% of one or more polyols.

In one embodiment, the paste prior to drying comprises more than about 1% of one or more polyols, such as more than about 2% of one or more polyols, for example more than about 3% of one or more polyols, such as more than about 4% of one or more polyols, for example more than about 5% of one or more polyols, such as more than about 6% of one or more polyols, for example more than about 7% of one or more polyols, such as more than about 8% of one or more polyols, for example more than about 9% of one or more polyols, such as more than about 10% of one or more polyols.

In one embodiment, the paste prior to drying comprises less than about 20% of one or more polyols, such as less than about 18% of one or more polyols, for example less than about 17% of one or more polyols, such as less than about 16% of one or more polyols, for example less than about 15% of one or more polyols, such as less than about 14% of one or more polyols, for example less than about 13% of one or more polyols, such as less than about 12% of one or more polyols, for example less than about 11% of one or more polyols, such as less than about 10% of one or more polyols.

After drying, the dry composition comprises from about 10% to about 60% of one or more polyols, such as from about 20% to about 50% of one or more polyols, such as from about 20% to about 45% of one or more polyols, for example from about 20% to about 40%, such as from about 20% to about 35% of one or more polyols, for example from about 20% to about 30% of one or more polyols.

In one embodiment, the dry composition comprises from about 20% to about 60% of one or more polyols, such as from about 20% to about 50% of one or more polyols, for example from about 20% to about 50%, such as from about 20% to about 45% of one or more polyols, for example from about 20% to about 40%, such as from about 20% to about 30% of one or more polyols.

In one embodiment, the dry composition comprises from about 25% to about 60% of one or more polyols, such as from about 25% to about 50% of one or more polyols, for example from about 25% to about 45% of one or more polyols, such as from about 25% to about 40% of one or more polyols, for example from about 25% to about 35% of one or more polyols, such as from about 25% to about 30% of one or more polyols.

In one embodiment, the dry composition comprises from about 27% to about 60% of one or more polyols, such as from about 27% to about 50% of one or more polyols, for example from about 27% to about 45% of one or more polyols, such as from about 27% to about 40% of one or more polyols, for example from about 27% to about 35% of one or more polyols, such as from about 27% to about 30% of one or more polyols.

In one embodiment, the dry composition comprises from about 30% to about 60% of one or more polyols, such as from about 30% to about 50% of one or more polyols, for example from about 30% to about 45% of one or more polyols, such as from about 30% to about 40% of one or more polyols, for example from about 30% to about 35% of one or more polyols.

In one embodiment, the dry composition comprises less polyol than biocompatible polymer, i.e. the polyol:biocompatible polymer ratio is less than 1:1, such as less than or about 0.9:1, for example less than or about 0.8:1, such as less than or about 0.7:1, for example less than or about 0.6:1, such as less than or about 0.5:1, such as less than or about 0.4:1, for example less than or about 0.3:1, such as less than or about 0.2:1, for example less than or about 0.1:1. The polyol:biocompatible polymer ratio is the same in the paste prior to drying.

In one embodiment, the polyol:biocompatible polymer ratio is between about 0.1:1 and 1:1; such as between about 0.2:1 and 1:1, for example between about 0.3:1 and 1:1, such as between about 0.4:1 and 1:1.

In a preferred embodiment, the polyol:biocompatible polymer ratio is between about 0.2:1 and 0.8:1; such as between about 0.2:1 and 0.7:1, for example between about 0.2:1 and 0.6:1, such as between about 0.2:1 and 0.5:1. Even more preferred, the polyol:biocompatible polymer ratio is between about 0.3:1 and 0.8:1; such as between about 0.3:1 and 0.7:1, for example between about 0.3:1 and 0.6:1, such as between about 0.3:1 and 0.5:1, for example between about 0.35:1 and 0.5:1, such as between about 0.35:1 and 0.45:1.

In one embodiment the polyol is not polyethylene glycol.

Extrusion Enhancer

It has previously been shown that the provision of certain extrusion enhancers, such as albumin in an appropriate amount, enables the use of higher gelatine concentrations as it decreases the amount of force needed to extrude the gelatine paste composition from e.g. a syringe. The use of higher gelatine concentrations may in turn improve the haemostatic properties of such products. It is necessary to provide the extrusion enhancers in appropriate amounts. The amounts shall be high enough so as to obtain the extrusion effect, i.e. to enable a flowable paste even for relatively high amounts of the biocompatible polymer, e.g. cross-linked gelatine, so that the haemostatic paste composition can be accurately applied by a surgeon using e.g. a syringe comprising an applicator tip; on the other hand, the amounts shall be as low as to prevent negative functional properties of the haemostatic composition.

In a preferred embodiment, the extrusion enhancer is albumin, especially human serum albumin.

In the wet paste composition before drying, the extrusion enhancer, such as albumin, is preferably present in an amount of between about 0.1% to about 10%, such as between about 0.2% to about 8%, for example between about 0.3% to about 7%, preferably between about 0.5% to about 5%, more preferred between about 1% to about 4%.

In the dry composition, the extrusion enhancer such as albumin is preferably present in an amount of between about 0.3% to about 30%, such as between about 0.5% to about 25%, for example between about 1% to about 20%, preferably between about 2% to about 15%.

In one embodiment, the extrusion enhancer is not present in the dry composition, but is instead introduced into the paste composition during reconstitution. For example the extrusion enhancer may be present in the aqueous medium used for reconstitution of the paste, thereby obtaining a wet paste composition comprising the extrusion enhancer.

In one embodiment, the reconstituted wet paste composition being present in an applicator device suitable for dispensing compositions in paste form, such as a syringe, has a mean extrusion force of 40 N or below, preferably below 35 N, especially preferred below 30 N or even below 20 N. Extrusion force may be tested by suitable methods known in the art capable of measuring the force required to extrude a paste product from a syringe.

In one embodiment, the reconstituted wet paste composition has a mean extrusion force (employing the test method described in example 1 of WO 2013/060770) of 40 N or below, preferably below 35 N, especially preferred below 30 N or even below 20 N.

Another class of extrusion enhancers according to the present disclosure are phospholipids, such as phosphatidylcholine and -serine, or complex mixtures such as lecithins or soy bean oils.

Bioactive Agent

In one embodiment of the present disclosure, the dry composition comprises one or more bioactive agents. It is essential that the bioactive agent retains its bioactivity, i.e. that the bioactive agent is biologically active in the paste after reconstitution of the dry composition. Many bioactive agents are unstable in solution, particularly enzymes and other proteins that may be degraded or lose their secondary structure when water is present.

In one embodiment the bioactive agent stimulates wound healing and/or haemostasis, such as thrombin.

Conventionally, a thrombin solution is added to a gelatine powder to make a haemostatic paste directly at the surgical site at the time of need of the haemostatic paste, e.g. by using commercially available haemostatic kits such as Floseal and Surgiflo®. The thrombin solution must be made just prior to making the paste as thrombin in solution is very unstable and will self-degrade rapidly. The making of a thrombin solution at the surgical site is time consuming and involves a risk of making mistakes regarding the correct dilution of thrombin.

The method of the present disclosure allows for the addition of thrombin to a paste prior to drying, thereby resulting in a dry composition comprising thrombin, which upon reconstitution with a suitable aqueous medium, such as water, will comprise a desired amount of thrombin without the need for time-consuming and error-prone thrombin dilution steps and addition at the surgical site. That thrombin may be included in the dry composition constitutes a clear advantage over conventional methods for making haemostatic pastes.

The present inventor has previously shown that thrombin may be included in a paste and dried by freeze-drying according with essentially no loss of thrombin activity measured in the reconstituted paste.

Thrombin may be added to the paste prior to drying at a concentration in the range of about 100 IU/ml paste to about 500 IU/ml paste, such as about 150 IU/ml paste to about 450 IU/ml paste, for example about 200 IU/ml paste to about 400 IU/ml paste, such as about 250 IU/ml paste to about 350 IU/ml paste.

In one embodiment, the one or more bioactive agents can be e.g. thrombin or thrombin in combination with fibrinogen, or thrombin and fibrinogen in combination with Factor XIII, or thrombin and fibrinogen and Factor XIII in combination with tranexamic acid.

Thrombin is a “trypsin-like” serine protease protein that in humans is encoded by the F2 gene. Prothrombin (coagulation factor II) is proteolytically cleaved to form thrombin in the coagulation cascade, which ultimately results in the stemming of blood loss. Thrombin in turn acts as a serine protease that converts soluble fibrinogen into insoluble strands of fibrin, as well as catalyzing many other coagulation-related reactions. In the blood coagulation pathway, thrombin acts to convert factor XI to XIa, VIII to VIIIa, V to Va, and fibrinogen to fibrin.

A preferred bioactive agent is thrombin. In one embodiment, the thrombin is added as prothrombin.

In one embodiment, the dry composition comprises one or more bioactive agents that stimulate bone and/or tendon healing such as one or more growth factors selected from the group consisting of matrix metalloproteinases (MMPs), insulin-like growth factor 1 (IGF-I), platelet-derived growth factor (PDGF), vascular endothelial growth factor (VEGF), basic fibroblast growth factor (bFGF) and transforming growth factor beta (TGF-β).

In one embodiment, the dry composition comprises one or more Bone Morphogenetic Proteins (BMPs). Bone morphogenetic proteins (BMPs) are a subgroup of the TGF-β superfamily. Bone Morphogenetic Proteins (BMPs) are a group of growth factors also known as cytokines and as metabologens. Originally discovered by their ability to induce the formation of bone and cartilage, BMPs are now considered to constitute a group of pivotal morphogenetic signals, orchestrating tissue architecture throughout the body.

In one embodiment, the dry composition comprises one or more matrix metalloproteinases (MMPs). MMPs are zinc-dependent endopeptidases. MMPs have a very important role in the degradation and remodeling of the extracellular matrix (ECM) during the healing process after an injury. Certain MMPs including MMP-1, MMP-2, MMP-8, MMP-13, and MMP-14 have collagenase activity, meaning that, unlike many other enzymes, they are capable of degrading collagen I fibrils.

These growth factors all have different roles during the healing process. IGF-1 increases collagen and proteoglycan production during the first stage of inflammation, and PDGF is also present during the early stages after injury and promotes the synthesis of other growth factors along with the synthesis of DNA and the proliferation of cells. The three isoforms of TGF-β (TGF-β1, TGF-β2, TGF-β3) are known to play a role in wound healing and scar formation. VEGF is well known to promote angiogenesis and to induce endothelial cell proliferation and migration.

In one embodiment, the dry composition comprises flakes or particles of extracelluar matrix (ECM). ECM is the extracellular part of animal tissue that usually provides structural support to the animal cells in addition to performing various other important functions. ECM has been shown to have very beneficial effect in healing as it facilitates functional tissue regeneration.

The variety of biological agents that can be used in conjunction with the paste of the disclosure is vast. In general, biological agents which may be administered via the compositions disclosed herein include, without limitation, antiinfectives, such as antibiotics and antiviral agents; analgesics and analgesic combinations; antihelmintics; antiarthritics; anticonvulsants; antidepressants; antihistamines; antiinflammatory agents; antimigraine preparations; antineoplastics; antiparkinsonism drugs; antipsychotics; antipyretics, antispasmodics; anticholinergics; sympathomimetics; xanthine derivatives; cardiovascular preparations including calcium channel blockers and beta-blockers such as pindolol and antiarrhythmics; antihypertensives; diuretics; vasodilators, including general coronary, peripheral and cerebral; central nervous system stimulants; hormones, such as estradiol and other steroids, including corticosteroids; immunosuppressives; muscle relaxants; parasympatholytics; psychostimulants; naturally derived or genetically engineered proteins, polysaccharides, glycoproteins, or lipoproteins; oligonucleotides, antibodies, antigens, cholinergics, chemotherapeutics, radioactive agents, osteoinductive agents, cystostatics heparin neutralizers, procoagulants and hemostatic agents, such as prothrombin, thrombin, fibrinogen, fibrin, fibronectin, heparinase, Factor X/Xa, Factor VII/VIIa, Factor VIII/VIIIa, Factor IX/IXa, Factor XI/XIa, Factor XII/XIIa, Factor XIII/XIIIa, tissue factor, batroxobin, ancrod, ecarin, von Willebrand Factor, collagen, elastin, albumin, gelatin, platelet surface glycoproteins, vasopressin, vasopressin analogs, epinephrine, selectin, procoagulant venom, plasminogen activator inhibitor, platelet activating agents and synthetic peptides having haemostatic activity.

Further Compounds

The dry composition of the present disclosure may further comprise one or more of the following: DMSO (dimethyl sulfoxide), 2-Methyl-2,4-pentanediol (MPD) and/or one or more of the compounds mentioned in the table below.

Bulking agent Buffering agent Solubilising agent Miscellaneous Sugars/Sugar Citric acid Complexing agent: Tonicifying agent: alcohols: Sodium citrate Ethylediamine tetra acetic Sodium chloride Mannitol Potassium citrate acid (EDTA) Sucrose Lactose Tartaric acid Alpha cyclodextrin Mannitol Sucrose Sodium phosphate Hydroxypropyl-β- Dextrose Trehalose Tris base cyclodextrin (HP-β-CD) Sorbitol Tris HCl Glucose Tris acetate Raffinose Zinc chloride Sodium acetate Potassium acetate Arginine Amino acids: pH adjusting agent: Surfactants: Antimicrobial Arginine Hydrochloric acid polysorbate 80 agents: Glycine Sodium hydroxide Benzalkonium Histidine Meglumine chloride benzyl alcohol phenol m-cresol methyl paraben ethyl paraben Polymer: Co-solvents: Collapse Dextran Tert-butyl alcohol temperature Polyethylene Iso-propyl alcohol modifier: glycol Dichloromethane Dextran Ethanol Hydroxyethyl starch Acetone Ficoll Glycerol gelatin

In one embodiment, the dry composition of the present disclosure comprises one or more antimicrobial agents, such as one or more antibacterial agents.

In one embodiment, the dry composition of the present disclosure comprises benzalkonium chloride (BAC).

In one embodiment, the dry composition of the present disclosure does not comprise an antimicrobial agent.

Making a Paste

According to the method of the present disclosure, the biocompatible polymer, the extrusion enhancer and the one or more polyols are mixed with a suitable aqueous medium to obtain a paste. The mixing may be performed in any suitable way known to a person of skill, e.g. by mixing the contents manually or by using an electrical mixing apparatus, such as a hand mixer, a kitchen mixer or an industrial mixer.

Mixing of the paste can generally be performed at room temperature (20-25° C.). However, if thrombin or other enzymes are included in the paste, it is advisable to perform the mixing of the paste at chilled temperatures and/or within a short time period to avoid or decrease the proteolytic activity of thrombin, as it is well-known that thrombin is liable to self-degradation in solution. Hence, when thrombin or other proteolytic enzymes are to be included in the paste, the mixing of the paste may be performed at temperatures below room temperature, such as at about 2° C. to about 20° C., for example at about 2° C. to about 15° C., preferably at about 4° C.

Another or an additional way of preserving the thrombin bioactivity in the paste is to keep the time that thrombin is in a wet state, i.e. the mixing time, at a minimum. Hence, when thrombin or other proteolytic enzymes are to be included in the paste, the mixing of the paste is usually performed within about 5 minutes to about 10 hours, such as about 5 minutes to about 5 hours, for example about 5 minutes to about 2 hours, preferably about 5 minutes to about 1 hour.

The present inventor has previously found that it is not essential to perform the mixing of the paste at low temperatures to avoid loss of thrombin activity as no decrease in thrombin activity was discovered when mixing of the paste was performed at ambient temperatures.

Containers

Any suitable container known to a person of skill may be used for preparing the paste and holding the paste while drying, such as vials, jars, tubes, trays, cartridges or syringes.

In one embodiment, the paste is prepared in one container and transferred to another container for drying, wherein said other container may be selected from a vial, a jar, a tube, a tray, a cartridge and a syringe.

A “jar” according to the present disclosure is a rigid, approximately cylindrical container with a wide mouth opening. Jars may comprise a re-closable closure unit/lid applied to the mouth of the jar.

The containers may be made from any suitable material such as glass, ceramic, plastic or metal, such as stainless steel.

Examples of suitable plastic materials include but are not limited to polyethylene, polypropylene, polystyrene, polyvinyl chloride, and polytetrafluoroethylene (PTFE).

In one embodiment, the paste is filled into and dried within a syringe or other known applicators suitable for dispensing flowable haemostatic compositions.

In one embodiment, the paste is dried within an applicator suitable for dispensing compositions in paste form, such as a syringe. Thus, in one embodiment, the present disclosure relates to an applicator, such as a syringe, comprising a dry composition contained therein.

The dry composition of the present disclosure may be prepared in various shapes, forms and sizes depending on the shape of the container used. They may be e.g. in the form of plugs, disks, rods, tubes, conical cylinders, sheets, spheres, half spheres, tablets, pellets, granules, or even fine particulates or powders (pulverised).

Haemostatic Sheet

In one embodiment the dry composition is in the form of a sheet, i.e. a substantially flat composition.

A dry composition in the form of a sheet may be obtained by spreading the paste thinly and evenly on a surface followed by drying of the paste to obtain a substantially flat dry sheet composition. A dry composition in the form of a sheet will upon contact with a liquid reconstitute spontaneously to form a paste. Thus, a dry composition in the form of a sheet has the advantages of both traditionally used surgical sponges in that it can cover relatively large areas and the advantage of a paste in that it, when wetted, conforms easily to uneven surfaces upon wetting.

The dry composition in the form of a sheet is soft and flexible.

In one embodiment the present disclosure relates to a dry composition in the form of a sheet for use in haemostasis and/or wound healing.

In one embodiment, the sheet is not pre-wetted before use, i.e. before application to a wound.

The height of the dry sheet composition is in one embodiment between about 0.5 mm and about 10 mm, preferably between about 1 mm and 5 mm, more preferred between about 1 mm and 3 mm, such as about 2 mm.

The size (width and depth) of the dry sheet composition depends on the intended use of the sheet and can be selected by the skilled person. The dry sheet material may e.g. be rectangular, square or circular. For example, the dry sheet composition may e.g. be in the form of a rectangle of approximately 5 cm×10 cm, 2 cm×6 cm, 6 cm×8 cm or 8 cm×12 cm.

In one embodiment, the dry sheet composition is cut into the desired shape prior to use.

Drying the Paste

According to the present disclosure the paste is dried to obtain the dry composition. The paste may be dried by any suitable methods known to a person of skill. Examples of suitable drying methods include freeze-drying and spray drying.

In one embodiment, the paste is frozen prior to the drying step.

In a preferred embodiment, the paste is freeze-dried. Any suitable freeze-drying technique and equipment known to the person of skill may be used.

Freeze-drying (also known as lyophilisation and cryodesiccation) is a dehydration process typically used to preserve a perishable material or make the material more convenient for transport. Freeze-drying works by freezing the material and then reducing the surrounding pressure to allow the frozen water in the material to sublimate directly from the solid phase to the gas phase.

There are essentially three categories of freeze-dryers: the manifold freeze-dryer, the rotary freeze-dryer and the tray style freeze-dryer. Two components are common to all types of freeze-dryers: a vacuum pump to reduce the ambient gas pressure in a vessel containing the substance to be dried and a condenser to remove the moisture by condensation on a surface cooled to −40 to −80° C. The manifold, rotary and tray type freeze-dryers differ in the method by which the dried substance is interfaced with a condenser. In manifold freeze-dryers a short usually circular tube is used to connect multiple containers with the dried product to a condenser. The rotary and tray freeze-dryers have a single large reservoir for the dried substance.

Rotary freeze-dryers are usually used for drying pellets, cubes and other pourable substances. The rotary dryers have a cylindrical reservoir that is rotated during drying to achieve a more uniform drying throughout the substance. Tray style freeze-dryers usually have rectangular reservoir with shelves on which products, such as pharmaceutical solutions and tissue extracts, can be placed in trays, vials and other containers.

Manifold freeze-dryers are usually used in a laboratory setting when drying liquid substances in small containers and when the product will be used in a short period of time. A manifold dryer will dry the product to less than 5% moisture content. Without heat, only primary drying (removal of the unbound water) can be achieved. A heater must be added for secondary drying, which will remove the bound water and will produce a lower moisture content.

Tray style freeze-dryers are typically larger than the manifold dryers and are more sophisticated. Tray style freeze-dryers are used to dry a variety of materials. A tray freeze-dryer is used to produce the driest product for long-term storage. A tray freeze-dryer allows the product to be frozen in place and performs both primary (unbound water removal) and secondary (bound water removal) freeze-drying, thus producing the dryest possible end-product. Tray freeze-dryers can dry products in bulk or in vials or other containers. When drying in vials, the freeze-drier is supplied with a stoppering mechanism that allows a stopper to be pressed into place, sealing the vial before it is exposed to the atmosphere. This is used for long-term storage, such as vaccines.

Improved freeze drying techniques are being developed to extend the range of products that can be freeze dried, to improve the quality of the product, and to produce the product faster with less labour.

Ever since the 1930s, industrial freeze drying has been dependent on a single type of equipment: the tray freeze drier. In 2005 a quicker and less-labour intensive freeze drying method was developed for bulk materials. This freeze drying process proved to be able to produce free-flowing powder from a single vessel. Known as [Active Freeze Drying] AFD technology, the new process used continuous motion to improve mass transfer and hence cutting processing time, while also eliminating the need to transfer to and from drying trays and downstream size reduction devices.

There are four stages in the complete freeze-drying process: pre-treatment, freezing, primary drying, and secondary drying.

Pre-treatment includes any method of treating the product prior to freezing. This may include concentrating the product, formulation revision (i.e., addition of components to increase stability and/or improve processing), decreasing a high vapor pressure solvent or increasing the surface area. In many instances the decision to pre-treat a product is based on theoretical knowledge of freeze-drying and its requirements, or is demanded by cycle time or product quality considerations. Methods of pre-treatment include: Freeze concentration, Solution phase concentration, Formulation to Preserve Product Appearance, Formulation to Stabilize Reactive Products, Formulation to Increase the Surface Area, and Decreasing High Vapor Pressure Solvents.

In a lab, freezing is often done by placing the material in a freeze-drying flask and rotating the flask in a bath, called a shell freezer, which is cooled by mechanical refrigeration, dry ice and methanol, or liquid nitrogen. On a larger scale, freezing is usually done using a freeze-drying machine. In this step, it is important to cool the material below its triple point, the lowest temperature at which the solid and liquid phases of the material can co-exist. This ensures that sublimation rather than melting will occur in the following steps. Larger crystals are easier to freeze-dry. To produce larger crystals, the product should be frozen slowly or can be cycled up and down in temperature. This cycling process is called annealing. In other cases it is better that the freezing is done rapidly, in order to lower the material to below its eutectic point quickly, thus avoiding the formation of ice crystals. Usually, the freezing temperatures are between −40° C. and −80° C. The freezing phase is the most critical in the whole freeze-drying process, because the product can be spoiled if badly done.

Amorphous materials do not have a eutectic point, but they do have a critical point, below which the product must be maintained to prevent melt-back or collapse during primary and secondary drying.

During the primary drying phase, the pressure is lowered (to the range of a few millibars or less), and enough heat is supplied to the material for the water to sublime. The amount of heat necessary can be calculated using the sublimating molecules' latent heat of sublimation. In this initial drying phase, about 95% of the water in the material is sublimated. This phase may be slow (can be several days in the industry), because, if too much heat is added, the material's structure could be altered.

In this phase, pressure is controlled through the application of partial vacuum. The vacuum speeds sublimation, making it useful as a deliberate drying process. Furthermore, a cold condenser chamber and/or condenser plates provide a surface(s) for the water vapour to re-solidify on. This condenser plays no role in keeping the material frozen; rather, it prevents water vapor from reaching the vacuum pump, which could degrade the pump's performance. Condenser temperatures are typically below −50° C.

It is important to note that, in this range of pressure, the heat is brought mainly by conduction or radiation; the convection effect is negligible, due to the low air density.

The vapour pressure of water is the pressure at which water vapour is saturated. At higher pressures water would condense. The water vapour pressure is the partial pressure of water vapour in any gas mixture saturated with water. The water vapour pressure determines the temperature and pressure necessary for freeze-drying to occur.

Vapour Pressure of Water (mTorr=Millitorr; mB=Millibar)

Temp (C.) mTorr mB 0 4579 6.104 −4 3280 4.372 −8 2326 3.097 −12 1632 2.172 −16 1132 1.506 −20 930 1.032 −24 526 0.6985 −28 351 0.4669 −32 231 0.3079 −36 150 0.2020 −40 96.6 0.1238 −44 60.9 0.0809 −48 37.8 0.0502 −52 23.0 0.0300 −56 13.8 0.0183 −60 8.0 0.0107 −64 4.6 0.0061 −68 2.6 0.0034 −72 1.4 0.0018

The secondary drying phase aims to remove unfrozen water molecules, since the ice was removed in the primary drying phase. This part of the freeze-drying process is governed by the material's adsorption isotherms. In this phase, the temperature is raised higher than in the primary drying phase, and can even be above 0° C., to break any physico-chemical interactions that have formed between the water molecules and the frozen material. Usually the pressure is also lowered in this stage to encourage desorption (typically in the range of microbars). However, there are products that benefit from increased pressure as well.

After the freeze-drying process is complete, the vacuum may be broken with an inert gas, such as nitrogen, before the material is sealed.

At the end of the operation, the final residual water content in the freeze-dried product is in general very low, such as around 2% or lower.

The freeze-drying process transforms the paste into a hard “cake-like” composition, which upon addition of an adequate amount of an aqueous medium, such as water, will form a ready-to use paste spontaneously, i.e. no mechanical mixing/reconstitution is required for said paste to form.

In one embodiment, the hard cake-like structure obtained by freeze-drying the paste is pulverised before addition of the aqueous medium.

In an alternative embodiment, the dry composition of the present disclosure is obtained by spray-drying. Any spray drying technique and equipment known to the skilled person may be applied.

Spray drying is a method of producing a dry powder from a liquid or slurry by rapidly drying with a hot gas. Air is usually the heated drying media; however, if the liquid is a flammable solvent such as ethanol or the product is oxygen-sensitive then nitrogen is used.

All spray dryers use some type of atomizer or spray nozzle to disperse the liquid or slurry into a controlled drop size spray. The most common of these are rotary disks and single-fluid high pressure swirl nozzles. Alternatively, for some applications two-fluid or ultrasonic nozzles are used. Depending on the process needs, drop sizes from 10 to 500 μm can be achieved with the appropriate choices. The most common applications are in the 100 to 200 μm diameter range. The dry powder obtained is often free-flowing.

Spray dryers can dry a product very quickly compared to other methods of drying. They also turn a solution or slurry into a dried powder in a single step, which can be advantageous for profit maximization and process simplification.

Outer Packaging

In one embodiment the dry composition contained within e.g. a syringe or other containment unit, is further contained within an outer packaging so that the dry product is kept sterile until use. This will allow the user to remove the outer packaging and transfer the dry composition into a sterile field. Here a suitable amount of aqueous medium can be added, whereupon a ready-to-use paste forms spontaneously within seconds without any need for mechanical agitation, stirring or mixing.

The outer packaging is usually made from a flexible, semi-rigid or rigid material and typically consists of materials such as plastic, aluminium foil and/or plastic laminate, where the plastic may be selected from the group consisting of PET, PETG, PE, LLDPE, CPP, PA, PETP, METPET, Tyvek and optionally bonded with an adhesive, such as polyurethane, or co-extruded.

In one embodiment, the outer packaging is an aluminium foil outer packaging.

The outer packaging preferably forms a complete barrier to moisture.

The outer packaging is preferably able to endure sterilisation treatment such as by radiation.

Sterilisation

The dry composition of the present disclosure is preferably sterile. Any suitable sterilisation technique known in the art may be utilised. The sterilisation preferably occurs after the packaging step, i.e. when the dry composition is contained within an outer packaging. Thus, in a preferred embodiment sterilisation is terminal sterilisation.

Sterilisation refers to any process that effectively kills or eliminates transmissible agents (such as fungi, bacteria, viruses, prions and spore forms etc.). Sterilisation of the dry composition can be achieved through e.g. application of heat, chemicals, and irradiation. Heat sterilization include autoclaving (uses steam at high temperatures) and dry heat; radiation sterilisation include X-rays, gamma and beta rays, UV light and subatomic particles; chemical sterilisation include using ethylene oxide gas, ozone, chlorine bleach, glutaraldehyde, formaldehyde, ortho phthalaldehyde, hydrogen peroxide and peracetic acid.

In one embodiment, the dry composition is sterilised by irradiation, e.g. ionizing irradiation, so as to provide sterility to the composition. Such irradiation may include e-beam (beta irradiation) or gamma irradiation. The level of irradiation and conditions for sterilisation, including the time that the composition is irradiated, are those that provide sterile compositions. Sterilisation conditions are similar to those currently utilized in the preparation of haemostatic loose powders currently available. Once having the benefit of this disclosure, one skilled in the art will be able to readily determine the level of irradiation necessary to provide sterile compositions.

When thrombin and/or other sensitive bioactive agents are present in the dried product, sterilisation is usually performed as terminal sterilisation with about 25 kGy or less of beta or gamma irradiation.

In one embodiment, sterilisation is performed with ethylene oxide.

Sterilisation with dry heat may typically be carried out by heating the dry composition to a temperature between 100° C. and 250° C., such as about 110° C. to about 200° C. In particular the temperature may be in the range of 110-160° C., e.g. in the range of 110-140° C., or in the range of 120-180° C., or in the range of 130-170° C., or in the range of 130-160° C., or in the range of 120-150° C.

In one embodiment, the dry composition is not sterilised after packaging. When the dry composition is manufactured by aseptic production techniques, the product is already sterile when placed in the outer packaging and no further sterilisation is required. Thus, in one embodiment the present disclosure relates to a composition produced by aseptic techniques.

Reconstitution of the Dry Composition

The dry composition of the present disclosure may be reconstituted by addition of a suitable amount of an aqueous medium. The aqueous medium used to reconstitute the paste may e.g. be selected from water, saline, a CaCl₂ solution or a buffered aqueous solution.

In one embodiment, the aqueous medium used to reconstitute the dry composition is water. In one embodiment, the tonicity of the aqueous medium is selected so that the tonicity of the reconstituted paste is compatible with use on human subjects in surgical procedures.

In one embodiment, the aqueous medium used to reconstitute the dry composition is saline.

In one embodiment, the aqueous medium used to reconstitute the dry composition comprises an extrusion enhancer, such as albumin. In this case, the dry composition preferably does not contain an extrusion enhancer.

Upon addition of the aqueous medium, a ready-to-use flowable paste forms spontaneously, i.e. within few seconds. Importantly, no mixing is required for the paste to form.

In one embodiment, the reconstituted paste contains a lower concentration of biocompatible polymer than the paste prior to drying due to the addition of more water than was removed from the paste during the drying step.

In one embodiment, the present disclosure relates to a method for reconstituting a dry composition comprising the steps of:

-   -   a. providing a dry composition as described herein, optionally         comprising an extrusion enhancer, and     -   b. adding an aqueous medium to the dry composition.

The aqueous medium may optionally comprise an extrusion enhancer such as albumin.

The extrusion enhancer may be present in the dry composition and/or in the reconstitution liquid, i.e. the aqueous medium.

In some embodiments the reconstituted paste comprises a similar concentration of polymer, e.g. gelatine, as conventionally used flowable paste compositions, but, due to the presence of the extrusion enhancer, the reconstituted paste of the present disclosure will be comparably easier to extrude from the applicator, e.g. a syringe.

In one embodiment, the reconstituted paste comprises a higher amount of biocompatible polymer than conventionally used flowable paste formulations. The increased amount of polymer may lead to an improved haemostatic effect, while still allowing for facile extrusion of the paste from e.g. a syringe.

In one embodiment, the reconstituted paste of the present disclosure comprises between about 10% to about 25% of the biocompatible polymer, for example between about 10% to about 20% of the biocompatible polymer, such as between about 12% to about 18% of the biocompatible polymer, for example between about 14% to about 16% of the biocompatible polymer, such as about 15% of the biocompatible polymer.

In one embodiment, the reconstituted paste of the present disclosure comprises less than about 15% of the biocompatible polymer, for example between about 10% to about 15% of the biocompatible polymer, such as between about 11% to about 15% of the biocompatible polymer, for example between about 12% to about 15% of the biocompatible polymer, such as between about 13% to about 15% of the biocompatible polymer, for example between about 14% to about 15% of the biocompatible polymer.

In one embodiment, the reconstituted paste of the present disclosure comprises more than about 15% of the biocompatible polymer, such as between about 15% to about 25% of the biocompatible polymer, for example between about 15% to about 20% of the biocompatible polymer, such as between about 16% to about 20% of the biocompatible polymer, for example between about 17% to about 20% of the biocompatible polymer, such as between about 18% to about 20% of the biocompatible polymer.

Medical Use

The present disclosure further relates to use of the dry composition or the paste obtained from the dry composition for promoting haemostasis and/or wound healing.

The paste of the present disclosure may e.g. be used in an array of surgical procedures wherein bleeding control is desired. A paste conforms to irregular surfaces to stop bleeding fast and it is therefore useful for providing rapid haemostasis on rough or uneven surfaces where haemostatic sponges are not efficient.

Haemostatic pastes are prepared directly at the surgical site at the time of need by the medical practitioner, i.e. doctors or nurses. The paste is thus often prepared under extremely stressful conditions and it is therefore essential that the process for preparing the paste is simple and fast to ensure that the bleeding is arrested as quickly as possible and that no mistakes are made while preparing the paste. It is also important that the consistency of the paste is suitable for use as a haemostatic paste, that the paste results in efficient and fast haemostasis and that the paste extrudes easily from the applicator device so that the surgeon applying the paste can administer the paste precisely to a site of bleeding without using excessive force.

The paste of the present disclosure is superior to currently available pastes such as Floseal and Surgiflo due to the fact that the paste of the present disclosure may be prepared simply by adding an amount of an aqueous medium to the dry composition, whereupon a ready-to-use haemostatic paste forms spontaneously, i.e. within less than about 30 seconds, preferably within less than about 20 seconds, more preferred within less than about 10 seconds, even more preferred within less than about 5 seconds.

The quantity of liquid to be added to the dry composition may be adjusted by the skilled person. The paste so formed always has an optimal consistency when the correct amount of liquid is added. This is not always the case with the conventional pastes, where the consistency of the paste may depend on the force applied and time spent mixing. That no mechanical mixing is required also means that less time is spent preparing the paste, which in turn leads to increased patient safety, both due to the fact that the haemostatic paste can be applied to the patient faster and that the simple preparation method decreases the likelihood of mistakes being made during the preparation of the haemostatic paste.

When thrombin is comprised within the dry composition, the disclosure further has the advantage over conventional pastes in that it avoids the time-consuming and error-prone thrombin dilution and addition steps involved in current methods for making haemostatic pastes.

In one embodiment the present disclosure relates to a method for arresting bleeding/promoting haemostasis in an individual in need thereof by application of the dry composition or the reconstituted paste as disclosed herein to a site of bleeding.

The paste of the present disclosure may be used for any type of surgery including general surgery, cardiothoracic surgery, vascular surgery, plastic surgery, paediatric surgery, colorectal surgery, transplant surgery, surgical oncology, trauma surgery, endocrine surgery, breast surgery, skin surgery, otolaryngology, gynaecology, oral and maxillofacial surgery, dental Surgery, orthopaedic surgery, neurosurgery, ophthalmology, podiatric surgery, urology.

In one embodiment the present disclosure relates to a method for promoting wound healing in an individual in need thereof by application of the dry composition or paste of the present disclosure to the wound.

A “wound” refers broadly to injuries to the skin and/or underlying (subcutaneous) tissue initiated in different ways (e.g., pressure sores from extended bed rest and wounds induced by trauma) and with varying characteristics. Wounds may be classified into one of four grades depending on the depth of the wound: i) Grade I: wounds limited to the epithelium; ii) Grade II: wounds extending into the dermis; iii) Grade III: wounds extending into the subcutaneous tissue; and iv) Grade IV (or full-thickness wounds): wounds wherein bones are exposed (e.g., a bony pressure point such as the greater trochanter or the sacrum). The present disclosure relates to treatment of any type of wound mentioned above using the dry composition or reconstituted paste of the present invention.

The treatment of a wound can in principle result in healing of the wound or in accelerated healing of the wound. The accelerated healing can be a result of e.g. administration of a wound-healing promoting substance. Alternatively, the wound healing can be promoted by preventing bacterial or viral infection, or by reducing the risk of such an infection which would otherwise have prolonged the wound treatment process.

In one embodiment the present disclosure relates to a method for promoting bone and/or tendon and/or tissue healing in an individual in need thereof by application of the dry composition or paste of the present disclosure to the injured bone, tendon or tissue.

The “individual” referred to herein may be any mammal, including, but not limited to, mammals of the order Rodentia, such as mice and hamsters, and mammals of the order Logomorpha, such as rabbits. It is preferred that the mammals are from the order Carnivora, including Felines (cats) and Canines (dogs). It is more preferred that the mammals are from the order Artiodactyla, including Bovines (cows) and Swines (pigs) or of the order Perssodactyla, including Equines (horses). It is most preferred that the mammals are of the order Primates, Ceboids, or Simoids (monkeys) or of the order Anthropoids (humans and apes). An especially preferred mammal is the human.

Kit

The present disclosure further relates to a kit comprising the dry composition and an amount of aqueous medium matched to the amount of the dry composition so that upon addition of the aqueous medium, a paste of a suitable consistency will form spontaneously, i.e. within seconds. Preferably, the kit is for use in the promotion of haemostasis or for use in wound, bone, tendon and/or tissue healing in an individual in need thereof.

Hence, in one embodiment the present disclosure relates to a kit comprising:

-   -   a) a container comprising the dry composition obtained by the         method of the present disclosure,     -   b) a container comprising an aqueous medium, and     -   c) optionally an outer packaging.

The aqueous medium used to reconstitute the paste may be e.g. be selected from water, saline, a CaCl₂ solution or a buffered aqueous solution.

In one embodiment, the aqueous medium used to reconstitute the dry composition is water. In one embodiment, the tonicity of the aqueous medium is selected so that an essentially isotonic paste will form upon addition of the aqueous medium to the dry composition. The tonicity of the paste is usually selected so that it is compatible with surgical use.

In one embodiment, the aqueous medium used to reconstitute the dry composition is saline.

In one embodiment, the dry composition comprises thrombin.

In one embodiment, the aqueous medium used to reconstitute the dry composition comprises an extrusion enhancer, such as albumin. In this case, the dry composition preferably does not contain an extrusion enhancer.

EXAMPLES Example 1 Haemostatic Pastes Comprising Varying Amounts of Mannitol and Glycerol Materials

50 g Gelatine powder (milled crosslinked gelatine sponges) 200 ml buffer

Polyols 50% Benzalkoniumchloride (BAC)

0.9% Saline solution

x and y g Mannitol and Glycerol According to the Following Plan:

Formulation X: Mannitol Y: Glycerol [#] [g] [g] 1 20 3 2 5 3 3 12.5 5 4 12.5 5 5 20 5 6 5 7 7 5 5 8 20 7 9 12.5 3 10 12.5 7 11 0 0

Equipment

Freeze dryer: Leybold-Heraus, Lyovac GT2 or Christ Alpha 1-4 LSC

Mixer: Kenwood, Major KM616 Method Buffer Solution:

Add 2.0 g±0.1 g BAC (50%) to a 250 mL blue cap bottle Add 98.0 g±0.5 g saline solution to the BAC Mix for 2 minutes using magnetic stirring—this is the BAC stock solution Add 123.0 g±0.5 g glycerol to a 2000 mL measuring flask Add 10 g±0.5 g BAC stock solution Add saline to the 2000 mL mark Place a stopper in the flask and turn it upside down a few times Mix by magnetic stirring for 5±1 minutes

Paste:

Dissolve×g polyol(s) in 200 ml buffer solution under stirring in the mixer. Add 50 g gelatine powder and mix with the dissolved polyol(s) until a homogeneous paste is obtained, approximately 5 minutes. Mixing of the paste was performed at room temperature, approximately 20° C.

Freeze-Drying:

The resulting paste is filled into 10 ml single use plastic syringes (5.5 ml per syringe) and placed at −30° C. for minimum 4 h. The frozen paste is transferred to the freeze-dryer and freeze dried until dry for 15 h.

Reconstitution:

The dry composition is reconstituted by adding 8 ml of liquid to each syringe, i.e. the amount of water which was removed from the composition during the freeze drying process is added. No mechanical mixing or stirring was used. The water was simply added to the dry composition and the composition left untouched until a paste was re-formed.

Results

The different formulations were tested for time to reconstitution, i.e. the time needed for a paste suitable for haemostatic purposes to spontaneously form without mechanical agitation of any sorts. *Triplicate determination

Formulation X: Mannitol Y: Glycerol Time to [#] [g] [g] reconstitution [sec]* 1 20 3 4 2 5 3 15 3 12.5 5 8 4 12.5 5 8.5 5 20 5 5 6 5 7 10 7 5 5 20 8 20 7 4 9 12.5 3 5 10 12.5 7 4 11 0 0 55

Formulation 11 is a negative control. The consistency of the formulation 11 paste was clearly inferior to the consistency of the pastes containing mannitol and glycerol in varying amounts.

Formulation 5

Formulation 5 had a spontaneous reconstitution time of 5 seconds. The contents of formulation 5 are specified in the table below in the paste (wet) and the dried composition (dry) respectively.

Content wet Content dry Content wet Content dry Formulation 5 [g] [g] [%] [%] Gelatine 50.00 50.00 18.18 56.65 Mannitol 20.00 20.00 7.27 22.66 Glycerol 12.30 12.30 4.47 13.94 (buffer) Glycerol 5.00 5.00 1.82 5.67 (added) BAC 0.01 0.01 0.00 0.01 NaCl 0.01 0.01 0.00 0.01 H₂0 187.68 0.94 68.25 1.06 SUM 275.00 88.26 100 100

The total percentage of glycerol in formulation 5 in the paste was thus 6.29% and in the dried composition 19.61%.

The total polyol concentration, i.e. mannitol and glycerol, in the paste was 13.56% and after drying 42.27%.

The polyol:gelatine ratio in the dry composition was approximately 0.75:1.

Example 2 Mannitol and Glycerol

A paste was made, dried and reconstituted according to the method described in Example 1. The contents of the paste are shown in the table below.

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 60.05 Mannitol 20.00 20.00 7.41 24.02 Glycerol 12.30 12.30 4.56 14.77 (buffer) Glycerol 0 0 0 0 (added) BAC 0.01 0.01 0.00 0.01 NaCl 0.01 0.01 0.00 0.01 H₂0 187.68 0.94 69.51 1.13 SUM 270.00 83.26 100 100

The spontaneous reconstitution time of the paste made according to the table above was 6 seconds.

The total polyol concentration, i.e. mannitol and glycerol, in the paste was 11.97% and after drying 38.79%.

The polyol:gelatine ratio in the dry composition was approximately 0.65:1.

Example 3 Mannitol

A paste was made, dried and reconstituted according to the method described in Example 1 with the exception that water was used instead of the buffer solution of Example 1. The contents of the paste are shown in the table below.

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 70.42 Mannitol 20.00 20.00 7.41 28.17 H₂0 200.00 1.00 74.07 1.41 SUM 270.00 71.00 100 100

The spontaneous reconstitution time of the paste made according to the table above was 7 seconds.

The results of the present example show that a paste of a suitable consistency for haemostatic purposes can be obtained from a freeze dried paste comprising only gelatine, water and a single polyol, in this case mannitol.

The polyol:gelatine ratio in the dry composition was approximately 0.4:1.

Example 4 Trehalose and Glycerol

A paste was made, dried and reconstituted according to the method described in Example 1. The contents of the paste are shown in the table below.

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 60.05 Trehalose 20.00 20.00 7.41 24.02 Glycerol 12.30 12.30 4.56 14.77 (buffer) Glycerol 0 0 0 0 (added) BAC 0.01 0.01 0.00 0.01 NaCl 0.01 0.01 0.00 0.01 H₂0 187.68 0.94 69.51 1.13 SUM 270.00 83.26 100 100

The spontaneous reconstitution time of the paste made according to the table above was 8 seconds.

The total polyol concentration, i.e. trehalose and glycerol, in the paste was 11.97% and after drying 38.79%.

The polyol:gelatine ratio in the dry composition was approximately 0.65:1.

Example 5 Thrombin

Thrombin was included in the formulation 5 paste of Example 1 at a theoretical concentration of 2500 IU/product (8 ml). The paste was made at room temperature (approximately 20° C.) and mixed as described in Example 1.

The resulting paste was dried by freeze-drying and reconstituted as described in Example 1. The thrombin activity was measured in the reconstituted paste. The results are shown in the table below.

Thrombin Activity - Freeze-dried composition in syringe [IU/product] 2519.60 2884.94 2796.71 Mean activity: 2733.75

No loss of thrombin activity was measured in the reconstituted paste.

The results further show that it is not strictly necessary to perform the mixing of the paste at low temperatures to avoid loss of thrombin activity as no decrease in thrombin activity was found when mixing was performed at ambient temperatures.

Example 6 Different Polyols

Pastes comprising different polyols were made, dried and reconstituted essentially as described in Example 1 with the exception that H₂0 with BAC was used instead of the buffer of example 1. The contents of the paste are shown in the tables below.

Content wet Content dry Content wet Content dry [g] [g] [W/W %] [W/W %] Gelatine 50.00 50.00 18.52 70.41 Mannitol 20.00 20.00 7.41 28.17 BAC 0.01 0.01 0.00 0.01 H₂0 200 1.00 74.07 1.41 SUM 270.01 71.01 100 100

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 70.41 Xylitol 20.00 20.00 7.41 28.17 BAC 0.01 0.01 0.00 0.01 H₂0 200 1.00 74.07 1.41 SUM 270.01 71.01 100 100

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 70.41 Trehalose 20.00 20.00 7.41 28.17 BAC 0.01 0.01 0.00 0.01 H₂0 200 1.00 74.07 1.41 SUM 270.01 71.01 100 100

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 70.41 Maltitol 20.00 20.00 7.41 28.17 BAC 0.01 0.01 0.00 0.01 H₂0 200 1.00 74.07 1.41 SUM 270.01 71.01 100 100

Content wet Content dry Content wet Content dry [g] [g] [%] [%] Gelatine 50.00 50.00 18.52 70.41 Sorbitol 20.00 20.00 7.41 28.17 BAC 0.01 0.01 0.00 0.01 H₂0 200 1.00 74.07 1.41 SUM 270.01 71.01 100 100

The polyol:gelatine ratio in the dry compositions was approximately 0.4:1.

The spontaneous reconstitution time of the pastes comprising different polyols made according to the tables above is shown in the table below and in FIG. 2. The experiments were repeated 5 times for each polyol.

Reconstitution Time in Seconds:

Mannitol Xylitol Trehalose Maltitol Sorbitol 1 7 14 11 14 29 2 9 31 28 14 28 3 9 20 16 23 29 4 10 30 29 16 35 5 9 31 23 22 32 Average 8.8 25.2 21.4 17.8 30.6 Std 1.1 7.8 7.8 4.4 2.9

The experiment shows that different kinds of polyols can be used for making a freeze-dried gelatine paste that will reconstitute spontaneously upon addition of water. The reconstituted paste has a consistency suitable for direct use as a haemostatic paste. 

1. A method of preparing a dry composition suitable for use in haemostasis and wound healing comprising the sequential steps of: a. providing a biocompatible polymer in powder form, one or more polyols, an extrusion enhancer and an aqueous medium, b. mixing the biocompatible polymer, the one or more polyols, the extrusion enhancer and the aqueous medium to obtain a paste, and c. drying the paste.
 2. The method according to claim 1, wherein the extrusion enhancer is albumin, preferably human serum albumin.
 3. The method according to any of the preceding claims, wherein the paste prior to drying comprises the extrusion enhancer in an amount of between about 0.1% w/w to about 10% w/w, preferably between about 0.5% w/w to about 5.0% w/w.
 4. The method according to any of the preceding claims, wherein the dry composition comprises from about 10% w/w to about 60% w/w of one or more polyols, such as from about 20% w/w to about 50% w/w of one or more polyols, for example from about 20% w/w to about 40% w/w, such as from about 20% w/w to about 30% w/w of one or more polyols.
 5. The method according to any of the preceding claims, wherein the paste prior to drying comprises from about 3% w/w to about 20% w/w of one or more polyols, such as from about 3% w/w to about 18% w/w of one or more polyols, for example from about 3% w/w to about 17% w/w of one or more polyols, such as from about 3% w/w to about 16% w/w of one or more polyols, for example from about 3% w/w to about 15% w/w of one or more polyols.
 6. The method according to any of the preceding claims, wherein the biocompatible polymer is cross-linked.
 7. The method according to any of the preceding claims, wherein the biocompatible polymer is obtained from a cross-linked sponge.
 8. The method according to any of the preceding claims, wherein the biocompatible polymer is gelatine.
 9. The method according to any of the preceding claims, wherein the drying is freeze-drying.
 10. The method according to any of the preceding claims, wherein the paste prior to drying comprises: a. from about 5% w/w to about 20% w/w of one or more polyols, b. from about 0.5% w/w to about 5% w/w of an extrusion enhancer, such as albumin, c. from about 15% w/w to about 25% w/w of biocompatible polymer, and d. from about 60% w/w to about 80% w/w of water.
 11. The method according to any of the preceding claims, wherein the dry composition comprises less than about 5% w/w of water, preferably less than about 3% w/w of water, more preferred less than about 2% w/w of water, such as less than about 1% w/w of water.
 12. The method according to any of the preceding claims, wherein the one or more polyols is selected from sugar alcohols, sugars and/or derivatives thereof.
 13. The method according to claim 12, wherein the one or more sugar alcohols is selected from the group consisting of glycol, glycerol, erythritol, threitol, arabitol, xylitol, ribitol, mannitol, sorbitol, dulcitol, fucitol, iditol, inositol, volemitol, isomalt, maltitol, lactitol and polyglycitol.
 14. The method according to any of the preceding claims, wherein the one or more polyols is mannitol and optionally one or more further polyols.
 15. The method according to any of the preceding claims, wherein the dry composition further comprises one or more bioactive agents that stimulate haemostasis or wound, bone, tendon and/or tissue healing.
 16. The method according to claim 15, wherein the bioactive agent is thrombin.
 17. The method according to any of the preceding claims, wherein the aqueous medium is selected from the group consisting of water, saline, a calcium chloride solution and a buffered aqueous medium.
 18. The method according to any of the preceding claims, wherein the method comprises a further step of placing the dry composition into an outer packaging, such as an aluminium foil packaging.
 19. The method according to any of the preceding claims, wherein the method comprises a further step of sterilising the dry composition.
 20. The method according to any of the preceding claims, wherein the paste is filled into and dried within an applicator suitable for dispensing compositions in paste form, such as a syringe.
 21. The method according to any of the preceding claims, wherein the dry composition reconstitutes to form a paste without mechanical mixing within less than about 30 seconds, preferably within less than about 20 seconds, more preferred within less than about 10 seconds, even more preferred within less than about 5 seconds.
 22. A dry composition obtained or obtainable by the method of any of the preceding claims.
 23. A dry composition comprising a biocompatible polymer, an extrusion enhancer such as albumin and one or more polyols.
 24. The dry composition according to claim 23, wherein the composition comprises: a. from about 10% w/w to about 60% w/w of one or more polyols, b. from about 0.3% w/w to about 30% w/w of an extrusion enhancer such as albumin, preferably about 2% w/w to about 15% w/w, c. from about 40% w/w to about 80% w/w of a biocompatible polymer, and d. from about 0.1% w/w to about 5% w/w of water.
 25. The dry composition according to any of claims 22 to 24, wherein the dry composition is present in an applicator suitable for dispensing compositions in paste form, such as a syringe.
 26. The dry composition according to any of claims 22 to 24, wherein the dry composition is in the form of a sheet.
 27. Use of the dry composition obtained by the method of any of claims 1 to 21 or the dry composition of any of claims 22 to 25 in the preparation of a paste.
 28. The dry composition obtained by the method of any of claims 1 to 21 or the dry composition of any of claims 22 to 26 for use in the promotion of haemostasis and/or wound, bone, tendon and/or tissue healing in an individual in need thereof.
 29. A kit comprising: a. a container comprising the dry composition obtained by the method of any of claims 1 to 21 or the dry composition according to any of claims 22 to 25, b. a container comprising an aqueous medium, and c. optionally an outer packaging.
 30. A method for reconstituting a dry composition comprising the steps of: a. providing a dry composition comprising a biocompatible polymer, one or more polyols, and optionally an extrusion enhancer such as albumin, b. adding an aqueous medium to the dry composition, wherein the aqueous medium optionally comprises an extrusion enhancer such as albumin, with the proviso that an extrusion enhancer is present in the dry composition and/or in the aqueous medium.
 31. The method according to claim 30, wherein the dry composition is as defined in any of claims 22 to
 26. 